WO2019167804A1 - Titanium cobble manufacturing method and manufacturing device - Google Patents
Titanium cobble manufacturing method and manufacturing device Download PDFInfo
- Publication number
- WO2019167804A1 WO2019167804A1 PCT/JP2019/006624 JP2019006624W WO2019167804A1 WO 2019167804 A1 WO2019167804 A1 WO 2019167804A1 JP 2019006624 W JP2019006624 W JP 2019006624W WO 2019167804 A1 WO2019167804 A1 WO 2019167804A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- particle size
- crusher
- crushing
- particles
- titanium
- Prior art date
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/14—Separating or sorting of material, associated with crushing or disintegrating with more than one separator
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/04—Magnetic separation acting directly on the substance being separated with the material carriers in the form of trays or with tables
- B03C1/08—Magnetic separation acting directly on the substance being separated with the material carriers in the form of trays or with tables with non-movable magnets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/02—Disintegrating by mills having rotary beater elements ; Hammer mills with horizontal rotor shaft
- B02C13/04—Disintegrating by mills having rotary beater elements ; Hammer mills with horizontal rotor shaft with beaters hinged to the rotor; Hammer mills
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/26—Details
- B02C13/282—Shape or inner surface of mill-housings
- B02C13/284—Built-in screens
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C21/00—Disintegrating plant with or without drying of the material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/30—Combinations with other devices, not otherwise provided for
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/28—Moving screens not otherwise provided for, e.g. swinging, reciprocating, rocking, tilting or wobbling screens
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/28—Moving screens not otherwise provided for, e.g. swinging, reciprocating, rocking, tilting or wobbling screens
- B07B1/36—Moving screens not otherwise provided for, e.g. swinging, reciprocating, rocking, tilting or wobbling screens jigging or moving to-and-fro in more than one direction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B08—CLEANING
- B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
- B08B15/00—Preventing escape of dirt or fumes from the area where they are produced; Collecting or removing dirt or fumes from that area
- B08B15/02—Preventing escape of dirt or fumes from the area where they are produced; Collecting or removing dirt or fumes from that area using chambers or hoods covering the area
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/005—Preliminary treatment of scrap
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/24—Binding; Briquetting ; Granulating
- C22B1/248—Binding; Briquetting ; Granulating of metal scrap or alloys
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1204—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 preliminary treatment of ores or scrap to eliminate non- titanium constituents, e.g. iron, without attacking the titanium constituent
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1218—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining titanium or titanium compounds from ores or scrap by dry processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C2201/00—Details of magnetic or electrostatic separation
- B03C2201/20—Magnetic separation whereby the particles to be separated are in solid form
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B2201/00—Details applicable to machines for screening using sieves or gratings
- B07B2201/04—Multiple deck screening devices comprising one or more superimposed screens
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F2009/001—Making metallic powder or suspensions thereof from scrap particles
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/20—Waste processing or separation
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
Definitions
- This disclosure relates to a titanium cobble manufacturing method and manufacturing apparatus.
- Patent Documents 1 and 2 Conventionally, a method of recycling by pulverizing and classifying wastes such as composite materials and iron-based waste raw materials has been known (see, for example, Patent Documents 1 and 2).
- titanium is used for various general uses and industrial uses because of its light weight, high strength, and high corrosion resistance.
- Such titanium has a limited production volume, and it is important to perform recycling.
- Patent Documents 1 and 2 do not disclose a method for producing titanium cobble from scrap material containing titanium.
- an object of the present disclosure is to provide a method and an apparatus for producing a large amount of titanium cobbles with a uniform particle size by pulverizing titanium scrap material while ensuring safety.
- a titanium cobble manufacturing method includes a preparation step of preparing a scrap material containing 50% by mass or more of metal titanium, and the first crushing of the scrap material.
- a first crushing step roughly crushing with a machine
- a second crushing step crushing the scrap material roughly crushed in the first crushing step with a second crusher
- the scrap material generated in the second crushing step A dust collection step for collecting fine dust, and a pulverized product of the scrap material generated in the second crushing step, medium particles having a particle size within a predetermined particle size range, and particles exceeding the particle size range
- scrap material containing 50% by mass or more of metal titanium is pulverized in two stages, thereby suppressing excessive frictional heat due to contact between metals and igniting during pulverization. Can be suppressed.
- fine dust that is easy to catch fire and can be the main cause of ignition in the dust collection process, it suppresses ignition of fine dust and reduces the temperature of fine dust even when sparks occur. Inflammation of the pulverized product or the like can be suppressed.
- classifying the pulverized product obtained by the two-stage crushing process into three types in the first classification process it is possible to produce a large amount of titanium cobbles having a uniform particle size with a high yield.
- a second technique is the first technique, wherein the scrap material is at least one selected from the group of a plate material, a tube material, a side trimming material, and a punching material, and the scrap material has a thickness of 3 mm or less, It is a waste material having a length of 1 m or less.
- the third technology is characterized in that, in the first or second technology, the first crusher is a biaxial crusher, and the second crusher is a hammer mill.
- a titanium cobble having a uniform particle size can be produced in a large amount with a high yield by two-stage crushing using a combination of a twin-screw crusher and a hammer mill.
- a first magnetic separation process for removing magnetized particles from the medium particles, and the large particles are returned to the second crushing process. And a return process.
- high-quality titanium cobbles can be manufactured with high yield by removing magnetic particles in the first magnetic separation process.
- the large particles obtained in the first classification step are returned again to the second crushing step, so that a sufficient amount of titanium cobble can be secured.
- a fifth technique is the collection process of collecting the fine dust and the small particles collected in the dust collecting process according to any one of the first to fourth techniques, and the collection of the fine dust and the small particles. It is characterized by comprising a second magnetic separation step of removing magnetism from the objects, and a second classification step of classifying the aggregate into at least two kinds.
- titanium cobbles having a smaller particle diameter can be obtained as a double product, and scrap materials can be effectively recycled.
- the sixth technology is characterized in that, in any one of the first to fifth technologies, the predetermined particle size range is 3 mm or more and 50 mm or less.
- a titanium cobble having a uniform particle size can be produced in a large amount with a high yield.
- a titanium cobble manufacturing apparatus includes a first crusher that roughly crushes a scrap material containing 50% by mass or more of titanium metal, and a crusher that crushes the scrap material roughly crushed by the first crusher.
- scrap material containing 50% by mass or more of metal titanium is pulverized in two stages of the first crusher and the second crusher, thereby suppressing the generation of excessive frictional heat.
- ignition during pulverization can be suppressed.
- fine dust that is easy to ignite and that can be the main cause of ignition with a dust collector, it suppresses the ignition of fine dust and reduces the temperature of fine dust even when sparks occur, and other pulverization Inflammation of products and the like can be suppressed.
- by classifying the pulverized product obtained by the two-stage pulverization into three types with a sieving machine it is possible to produce a large amount of titanium cobbles having a uniform particle size with a high yield.
- An eighth technique includes the first magnetic separator that removes magnetism from the medium particles in the seventh technique, and a conveyor device that returns the large particles to the second crusher. It is characterized by that.
- a sufficient production amount of titanium cobble can be ensured by returning the large particles obtained by the sieving machine to the second crusher again. Then, by removing the magnetic particles in the first magnetic separator, it is possible to manufacture high quality titanium cobbles with a high yield.
- a ninth technique is the vibration sieve machine according to the seventh or eighth technique, wherein the sieving machine includes two types of mesh materials having different hole diameters in upper and lower stages, and the upper mesh material has a hole diameter of 50 mm.
- the pore diameter of the lower mesh material is 3 mm, and the pulverized product is disposed on the upper mesh material.
- the particles can be classified effectively by the upper and lower two-stage mesh material, titanium cobbles having a uniform particle size can be produced in large quantities with a high yield.
- the scrap material containing 50% by mass or more of metal titanium is pulverized in two stages to suppress generation of excessive frictional heat due to contact between metals, and during pulverization. Can be suppressed.
- fine dust that is easy to catch fire and can be the main cause of ignition in the dust collection process, it suppresses ignition of fine dust and reduces the temperature of fine dust even when sparks occur. Inflammation of the pulverized product or the like can be suppressed.
- classifying the pulverized product obtained by the two-stage crushing process into three types in the first classification process it is possible to produce a large amount of titanium cobbles having a uniform particle size with a high yield.
- titanium cobble refers to titanium-containing particles having a longest diameter of 50 mm or less and a longest diameter divided by the shortest diameter and containing 50% by mass or more of metallic titanium.
- longest diameter refers to the maximum width of the outer shape of the particle
- shortest diameter refers to the minimum width of the outer shape of the particle
- the “particle size” of particles such as titanium cobble means the longest diameter of the particles.
- the titanium cobble manufacturing method includes a preparation step S1, a first crushing step S2, a second crushing step S3, a dust collection step S4, and a first classification step.
- S5 1st magnetic separation process S6, return process S7, collection process S8, 2nd magnetic selection process S9, and 2nd classification process S10 are provided.
- FIG. 2 shows an example of a manufacturing apparatus 1 for manufacturing titanium cobbles by the titanium cobble manufacturing method shown in FIG.
- the scrap material 11 roughly crushed by the first crusher 21 is conveyed by the first conveyor device 22, and is put into the second crusher 23 and crushed (second crushing step S3). ).
- a duct 27 a connected to the dust collector 27 is disposed on the upper part of the second crusher 23.
- the fine dust 410 generated when the scrap material 11 is pulverized by the second crusher 23 is sucked by the dust collector 27 and collected through the duct 27a (dust collection step S4).
- the fine dust 410 is sent to the collection part 27b arrange
- the scrap material 11 crushed by the second crusher 23 is fed into the inlet 245 of the first sieving machine 24 (sieving machine) as indicated by an arrow A4. And as shown by arrow A5, it sends to the sieve part 244 of the 1st sieve machine 24.
- FIG. The sieve portion 244 includes a first mesh 241 (upper mesh material), a second mesh 242 (lower mesh material), and a bottom portion 243.
- the scrap material 11 thrown into the insertion port 245 is, as shown by arrows A51, A52, A53 in FIGS. 1 and 2, large particles 411, medium particles 412, by the first mesh 241 and the second mesh 242. And small particles 413 (first classification step S5).
- the middle particles 412 are discharged from the second discharge port 24b of the first sieving machine 24 and input to the first magnetic separator 25 as indicated by an arrow A62. Then, the magnetic middle particle 51 having magnetism is removed from the middle particle 412 by the first magnetic separator 25, and the titanium cobble 41 as a product is obtained as indicated by an arrow A7 (first magnetic separation step S6). ).
- the large particles 411 are discharged from the first discharge port 24a of the first sieving machine 24 as shown by an arrow A63, and are put into the middle of the first conveyor device 22 by the second conveyor device 30 (conveyor device). It inputs into the 2nd crusher 23, ie, returns to 2nd crushing process S3 (return process S7).
- the small particles 413 are discharged from the third discharge port 24c of the first sieve 24 and sent to the collection unit 27b provided at the lower part of the dust collector 27 by the third conveyor device 26.
- the fine dust 410 collected by the dust collector 27 is collected (collecting step S8).
- the aggregate of the fine dust 410 and the small particles 413 is sent from the collecting unit 27b to the second magnetic separator 28 as indicated by an arrow A102. Then, as shown by the arrow A103, the magnetic assembly 52 having magnetism is removed from the assembly by the second magnetic separator 28 (second magnetic separation step S9).
- the aggregate from which the magnetic aggregate 52 has been removed is sent to the second sieving machine 29 as shown by an arrow A104, and as shown by arrows A105 and A106, a fine titanium cobble 42 and a small titanium cobble 43 (Second classification step S10).
- the preparation step S1 is a step of preparing the scrap material 11.
- the scrap material 11 is a waste material such as used scraps or processing scraps generated at a processing factory of a manufacturer and the like containing metal titanium in an amount of 50% by mass or more, more preferably 60% by mass or more, particularly preferably 80% by mass or more. is there.
- the type of the scrap material 11 is not particularly limited, and specific examples include a plate material, a tube material, a side trimming material, a punching material, a hole punching material, a coil material, and the like, preferably a plate material, a tube material, It is at least one selected from the group of side trimming materials and punching materials.
- examples of the plate material include waste materials such as a strip-shaped remaining portion remaining as a processing yield at the time of product manufacture.
- the tube material examples include waste materials generated when manufacturing parts for heat exchangers and seawater desalination plants.
- the side trimming material is, for example, a waste material generated when a plate material or the like is manufactured by cutting off an end portion of a titanium coil.
- the punched material is, for example, a remaining part after being punched, which is generated when a raw material plate or the like is punched into a closed product shape.
- the punched material is, for example, a punched portion that is generated when a raw material plate or the like is punched into a shape that is closed all around.
- the coil material is, for example, a waste material such as a defective product generated during cold rolling of a raw material plate material or a defective product having scratches, dents, or the like.
- the scrap material 11 has a thickness of 3 mm or less, preferably 0.4 mm or more and 2 mm or less, and a length of 1 m from the viewpoint of manufacturing a large amount of titanium cobbles 41 having a uniform particle size with high yield while ensuring safety.
- it is preferably 0.8 m (800 mm) or less.
- a tube outer diameter is 20 mm or less.
- the first crushing step S ⁇ b> 2 is a step of roughly crushing the scrap material 11 with the first crusher 21.
- the first crusher 21 roughly crushes the scrap material 11 so that the longest diameter is 500 mm or less, preferably 300 mm or less, more preferably 200 mm or less.
- the 1st crusher 21 if it is a crusher suitable for rough crushing of the scrap material 11, a well-known crusher can be utilized, for example, a uniaxial crusher, a biaxial crusher, a four axis
- the first crusher 21 When a biaxial crusher is employed as the first crusher 21, it is not particularly limited.
- the first crusher 21 includes a motor of 30 kW or more and 200 kW or less, and a horizontal sectional area of the crushing chamber (for example, a crushing chamber is If it is a rectangular parallelepiped, the thing of width x depth) is 0.2 m 2 or more and 6 m 2 or less, for example. Thereby, the crushing of the scrap material 11 can be performed effectively.
- the second crushing step S3 is a step of crushing the scrap material 11 roughly crushed by the first crusher 21, and is performed by the second crusher 23.
- the second crusher 23 crushes the scrap material 11 roughly crushed by the first crusher 21 so that the longest diameter is preferably 150 mm or less, more preferably 100 mm or less, and particularly preferably 80 mm or less.
- any known crusher can be used as long as it is a crusher suitable for crushing the scrap material 11.
- a hammer mill, a disc mill, a jet mill, a uniaxial A crusher, a biaxial crusher, a 4-axis crusher, etc. are mentioned. From the viewpoint of obtaining a titanium cobble 41 having a uniform particle size in a short time, it is particularly preferable to use a hammer mill as the second crusher 23.
- the second crusher 23 has a motor of 50 kW or more and 150 kW or less and has a horizontal sectional area of the crushing chamber (for example, the crushing chamber is a rectangular parallelepiped If it exists, the thing of width x depth) is 0.2 m 2 or more and 3 m 2 or less, for example.
- the hammer mill is provided with a mesh-like screen at the discharge portion of the pulverized product, and the mesh size of the screen is appropriately adjusted by replacing the screen according to the desired size of the pulverized product as described above.
- the upper limit is preferably 150 mm or less, more preferably 100 mm or less, and particularly preferably 80 mm or less.
- the lower limit of the mesh size of the screen is not particularly limited, but from the viewpoint of increasing the safety of the manufacturing apparatus 1 by shortening the pulverization time in the hammer mill, preferably 10 mm or more, more preferably 20 mm or more, Especially preferably, it is 30 mm or more.
- the scrap material 11 can be charged into the hammer mill according to the processing capacity such as the size of the hammer mill blade, the state of the hammer mill, the capacity of the crushing chamber, and the output of the motor.
- the horizontal sectional area 1 m 2 of the crushing chamber is preferably 5 kg / min or less, more preferably 3 kg / min or less, particularly preferably 2 kg / min or less. It is.
- the scrap material 11 is pulverized in two stages by the first crushing step S2 and the second crushing step S3, so that the scrap materials 11 and the inner walls and scrap of the first crusher 21 and the second crusher 23 are scraped.
- the amount of frictional heat generated due to contact with the material 11 can be suppressed, and safety during pulverization can be ensured.
- a titanium cobble having a uniform particle size can be produced in a large amount with a high yield in a short time.
- the time until the second crusher 23 is charged is the safety of the manufacturing apparatus 1 by suppressing the amount of frictional heat generated during crushing in the second crusher 23. From the viewpoint of enhancing the properties, it is preferably 2 minutes or longer, more preferably 3 minutes or longer, particularly preferably 4 minutes or longer.
- the dust collection step S ⁇ b> 4 is a step of collecting fine dust generated when the scrap material 11 is pulverized by the second crusher 23, and is performed by the dust collector 27.
- the dust collector 27 is, for example, a cyclone type dust collector that separates and collects fine dust by a swirling airflow or centrifugal force, a pulse jet type or a back filter type dust collector, and is preferably a cyclone type dust collector.
- the fine dust generated in the second crusher 23 is collected by the dust collector 27 through the duct 27a.
- the dust collector 27 When a cyclone type dust collector is adopted as the dust collector 27, among the fine dust 410 collected through the duct 27a, the one with a large specific gravity is sent to the collecting portion 27b, while the other fine dust with a small specific gravity is shown in FIG. It can be stored in an external dust bag.
- the pulverized product of the scrap material 11 generated in the second crushing step S3 has medium particles 412 having a particle size within a predetermined particle size range and a particle size exceeding the particle size range. This is a step of classifying the large particles 411 into small particles 413 having a particle size smaller than the particle size range.
- the predetermined particle size range can be appropriately set according to the desired particle size of the titanium cobble 41, but from the viewpoint of producing a large amount of titanium cobble with a uniform particle size with a high yield, the upper limit is preferably 50 mm or less. Is 30 mm or less, more preferably 25 mm or less, and the lower limit thereof is preferably 3 mm or more, more preferably 3.5 mm or more, and particularly preferably 4 mm or more.
- the particle size of the large particles 411 is more than 50 mm, preferably more than 30 mm, more preferably more than 25 mm.
- the particle size of the small particles 413 is preferably less than 3 mm, more preferably less than 3.5 mm, and particularly preferably less than 4 mm.
- the predetermined particle size range is set to 3 mm or more and 50 mm or less, for example.
- the large particles 411 have a particle size of more than 50 mm
- the medium particles 412 have a particle size of 3 mm or more and 50 mm or less
- the small particles 413 have a particle size of less than 3 mm.
- the first sieving machine 24 is a vibration sieving machine
- FIG. 3 is a schematic cross-sectional view showing an enlarged part of the sieving portion 244 of the first sieving machine 24.
- the sieve part 244 includes a first mesh 241, a second mesh 242, and a bottom part 243.
- the sieve portion 244 has a substantially U-shaped cross section in a direction perpendicular to the particle traveling direction (the direction of the arrow A51 in FIG. 2) and extends in the traveling direction, for example, an outer wall portion made of metal such as stainless steel. (Not shown), and the bottom portion 243 forms the bottom side of the outer wall portion.
- the first mesh 241 and the second mesh 242 are for separating the pulverized products of the scrap material 11 according to the particle diameter, and are formed by punching holes with a desired hole diameter in a metal plate made of stainless steel or the like. It is.
- the 1st mesh 241 and the 2nd mesh 242 are not restricted to such a structure, A metal net
- the 1st mesh 241 and the 2nd mesh 242 are attached to the attachment part provided in the upper and lower two steps
- the first mesh 241 and the second mesh 242 are two types of plate-shaped mesh materials having different hole diameters, and the sieve portion 244 includes the first mesh 241 and the second mesh 242 in two upper and lower stages.
- the hole diameter of the first mesh 241 is 50 mm, and the hole diameter of the second mesh 242 is 3 mm.
- the pulverized product charged into the inlet 245 of the first sieve 24 is sent onto the first mesh 241 as the first sieve 24 vibrates. Then, as shown in FIGS. 2 and 3, the large particles 411 having a longest diameter of 50 nm are sent out toward the first discharge port 24a while remaining on the first mesh 241.
- Medium particles 412 having a longest diameter of 3 mm or more and 50 mm or less and small particles 413 having a longest diameter of less than 3 mm are arranged on the lower side through the holes of the first mesh 241 in accordance with the vibration of the first sieve machine 24, and on the second mesh 242. Placed in.
- the medium particles 412 are sent out toward the second discharge port 24b while remaining on the second mesh 242.
- the small particles 413 are disposed on the bottom 243 disposed further down through the hole of the second mesh 242 along with the vibration of the first sieve 24 and are sent out toward the third discharge port 24c.
- the pulverized product can be classified effectively by the upper and lower two-stage first mesh 241 and second mesh 242.
- the titanium cobble 41 having a uniform particle diameter can be manufactured in a large amount with a high yield.
- the first discharge port 24 a on the terminal side of the first mesh 241 extends toward the second conveyor device 30.
- the first discharge port 24 a may be connected to the second conveyor device 30.
- the second discharge port 24 b on the terminal side of the second mesh 242 extends toward the first magnetic separator 25.
- the second discharge port 24b may be connected to the first magnetic separator 25.
- the hole diameters of the first mesh 241 and the second mesh 242 may be changed to those of the desired hole diameter.
- the predetermined particle size range is, for example, 5 mm or more and 30 mm or less
- the first mesh 241 and the second mesh 242 are changed from those having a hole diameter of 50 mm and 3 mm to those having a hole diameter of 30 mm and 5 mm, respectively. That's fine.
- the particle size of the titanium cobble 41 can be adjusted by changing the first mesh 241 and the second mesh 242 to those having different hole diameters.
- the first magnetic separation step S ⁇ b> 6 is a step of removing the magnetized particles from the medium particles 412 and is performed by the first magnetic separation machine 25.
- the middle particle 412 is divided into a product titanium cobble 41 and a magnetic middle particle 51 having magnetism as a by-product.
- the 1st magnetic separator 25 is not specifically limited, For example, general magnetic separators, such as a drum type and a counter-polar drum type, are employable.
- the quality of the titanium cobble 41 can be improved by removing the magnetic middle particles 51.
- the first magnetic separation step S6 is an optional step.
- the first magnetic separation step S6 is omitted when the scrap material 11 does not reliably include magnetism. can do.
- the medium particle 412 is obtained as a titanium cobble 41 as a product.
- the return step S ⁇ b> 7 is a step of returning the large particles 411 to the second crusher 23, and is performed by the second conveyor device 30. Thereby, the sufficient production amount of the titanium cobble 41 can be ensured by returning the large particles to the second crushing step S3 again.
- the return step S7 is an optional step and may not be provided, but is desirably provided from the viewpoint of sufficiently recycling the scrap material 11 and securing a sufficient production amount of the titanium cobble 41.
- the terminal part of the 2nd conveyor apparatus 30 is arrange
- the collection step S8 is a step of collecting the fine dust 410 collected in the dust collection step S4 and the small particles obtained in the first classification step S5.
- the collection step S8 is an optional step and may not be provided.
- the second magnetic separation step S ⁇ b> 9 is a step of removing the magnetized material from the aggregate of the fine dust 410 and the small particles 413, that is, the magnetic aggregate 52, and is performed by the second magnetic separator 28.
- the 2nd magnetic separator 28 is not specifically limited, The magnetic separator similar to the 1st magnetic separator 25 is employable.
- the first magnetic separator 25 and the second magnetic separator 28 may have the same configuration or different configurations.
- the second magnetic separation step S9 is an optional step and may not be provided. However, when the fine dust 410 and the small particles 413 are classified by the second classification step S10 to be recycled products, the second magnetic separation step S9 is performed. It is desirable to do.
- the second classification step S10 is a step of classifying the aggregate into at least two kinds, and is performed by the second sieve 29.
- the second sieving machine 29 may be, for example, a vibration sieving machine having the same configuration as the first sieving machine 24 or a circular sieving machine. Moreover, an ultrasonic vibration sieving machine may be used.
- the second classification step S10 is an optional step and may not be provided, but is desirably provided when the fine dust 410 and the small particles 413 are recycled as products.
- titanium cobbles having a smaller particle diameter can be obtained as a double product, and the scrap material 11 can be effectively recycled.
- 2nd classification process S10 although it is the structure classified into two types of fine titanium cobble 42 and the small titanium cobble 43, the structure classified into three or more types may be sufficient.
- the titanium cobble 41 obtained as described above is used for applications such as titanium ingot raw materials, super alloys, additives for aluminum alloys, steels, and the like.
- the yield of the titanium cobble 41 obtained by the manufacturing method according to the present embodiment is expressed as a percentage of the mass of the titanium cobble 41 to the mass of the scrap material 11, and is 70% or more, preferably 75% or more, particularly preferably 80% or more. It is. Further, the combined yield of the titanium cobble 41 and the fine titanium cobble 42 and the small titanium cobble 43 which are the products of the second classification step S10 is the ratio of the total mass of the titanium cobble 41, the fine titanium cobble 42 and the small titanium cobble 43 to the mass of the scrap material 11. Expressed as a percentage, it is 80% or more, preferably 85% or more, particularly preferably 90% or more.
- the time from when the scrap material 11 is put into the first crusher 21 until the titanium cobble 41 is obtained is within 1 hour, preferably within 40 minutes, in particular. Preferably it is within 30 minutes.
- the first sieving machine 24 is a vibration sieving machine.
- the second sieving machine 29 similarly to the second sieving machine 29, it may be a circular or drum type sieving machine, an ultrasonic sieving machine, or the like.
- the first sieving machine 24 includes a first mesh 241 and a second mesh 242 in two upper and lower stages, and the scrap material 11 crushed by the second crusher 23 is composed of large particles 411, medium particles 412, and small particles. Although it was the structure classified into 413, it is good also as a structure which is further provided with one or more mesh materials, for example, and classify
- titanium cobble products of various sizes can be manufactured by classifying finely according to various sizes.
- This disclosure is extremely useful because it can provide a method and an apparatus for pulverizing titanium scrap material and producing a large amount of titanium cobble with a uniform particle size with a high yield while ensuring safety.
Abstract
Description
<定義>
本明細書において、「チタンコブル」とは、金属チタンを50質量%以上含有する最長径50mm以下、最長径を最短径で除して得られるアスペクト比5以下のチタン含有粒子のことをいう。 (Embodiment 1)
<Definition>
In this specification, “titanium cobble” refers to titanium-containing particles having a longest diameter of 50 mm or less and a longest diameter divided by the shortest diameter and containing 50% by mass or more of metallic titanium.
図1に示すように、本開示の一実施形態に係るチタンコブルの製造方法は、準備工程S1と、第1破砕工程S2と、第2破砕工程S3と、集塵工程S4と、第1分級工程S5と、第1磁選工程S6と、リターン工程S7と、収集工程S8と、第2磁選工程S9と、第2分級工程S10とを備えている。 <Titanium Cobble Manufacturing Method and Manufacturing Apparatus>
As shown in FIG. 1, the titanium cobble manufacturing method according to an embodiment of the present disclosure includes a preparation step S1, a first crushing step S2, a second crushing step S3, a dust collection step S4, and a first classification step. S5, 1st magnetic separation process S6, return process S7, collection process S8, 2nd magnetic selection process S9, and 2nd classification process S10 are provided.
図2中矢印A1で示すように、図1の準備工程S1で準備されたスクラップ材11は、第1破砕機21に投入され、粗破砕される(第1破砕工程S2)。 <Outline of titanium cobble manufacturing process>
As shown by an arrow A1 in FIG. 2, the
以下、図1~図3を参照して、チタンコブルの製造工程の各構成について説明する。 <About each process>
In the following, with reference to FIG. 1 to FIG. 3, each structure of the titanium cobble manufacturing process will be described.
準備工程S1は、スクラップ材11を準備する工程である。 ≪Preparation process≫
The preparation step S1 is a step of preparing the
第1破砕工程S2は、スクラップ材11を第1破砕機21で粗破砕する工程である。 ≪First crushing process≫
The first crushing step S <b> 2 is a step of roughly crushing the
第2破砕工程S3は、第1破砕機21で粗破砕されたスクラップ材11を粉砕する工程であり、第2破砕機23により行われる。 ≪Second crushing process≫
The second crushing step S3 is a step of crushing the
集塵工程S4は、第2破砕機23によるスクラップ材11の粉砕時に生じる微粉塵を集塵する工程であり、集塵機27により行われる。 ≪Dust collection process≫
The dust collection step S <b> 4 is a step of collecting fine dust generated when the
第1分級工程S5は、第2破砕工程S3において生じたスクラップ材11の粉砕生成物を、所定の粒径範囲内の粒径を有する中粒子412と、該粒径範囲を超える粒径を有する大粒子411と、該粒径範囲よりも小さい粒径を有する小粒子413とに分級する工程である。 ≪First classification process≫
In the first classification step S5, the pulverized product of the
第1磁選工程S6は、中粒子412の中から磁性を帯びたものを取り除く工程であり、第1磁選機25により行われる。中粒子412は、本工程により、結果として、製品であるチタンコブル41と、副生成物として磁性を帯びた磁性中粒子51とに分けられる。第1磁選機25は、特に限定されるものではなく、例えばドラム型、対極式ドラム型等一般的な磁選機を採用することができる。 ≪First magnetic selection process≫
The first magnetic separation step S <b> 6 is a step of removing the magnetized particles from the
リターン工程S7は、大粒子411を第2破砕機23にリターンする工程であり、第2コンベア装置30により行われる。これにより、大粒子を再度第2破砕工程S3にリターンすることで、チタンコブル41の十分な製造量を確保することができる。 ≪Return process≫
The return step S <b> 7 is a step of returning the
収集工程S8は、集塵工程S4で集塵した微粉塵410と第1分級工程S5で得られた小粒子とを集める工程である。収集工程S8は任意の工程であり設けなくてもよい。微粉塵410及び小粒子413を第2分級工程S10により分級してリサイクル製品とする場合は、収集工程S8を行うことが望ましい。なお、収集工程S8を設ける場合は、収集部27bにおいて、微粉塵410及び小粒子413を混合し、均一化しておく構成としてもよい。 ≪Collection process≫
The collection step S8 is a step of collecting the fine dust 410 collected in the dust collection step S4 and the small particles obtained in the first classification step S5. The collection step S8 is an optional step and may not be provided. When the fine dust 410 and the
第2磁選工程S9は、微粉塵410及び小粒子413の集合物の中から磁性を帯びたもの、すなわち磁性集合物52を取り除く工程であり、第2磁選機28により行われる。第2磁選機28は、特に限定されるものではないが、第1磁選機25と同様の磁選機を採用することができる。なお、第1磁選機25及び第2磁選機28は同一の構成のものであってもよいし、異なる構成のものであってもよい。第2磁選工程S9は、任意の工程であり、設けなくてもよいが、微粉塵410及び小粒子413を第2分級工程S10により分級してリサイクル製品とする場合は、第2磁選工程S9を行うことが望ましい。 ≪Second magnetic selection process≫
The second magnetic separation step S <b> 9 is a step of removing the magnetized material from the aggregate of the fine dust 410 and the
第2分級工程S10は、集合物を少なくとも2種以上に分級する工程であり、第2ふるい機29により行われる。第2ふるい機29は、例えば第1ふるい機24と同様の構成の振動ふるい機であってもよいし、円形振動ふるい機であってもよい。また超音波振動ふるい機であってもよい。 ≪Second classification process≫
The second classification step S10 is a step of classifying the aggregate into at least two kinds, and is performed by the
上述のごとく得られたチタンコブル41は、チタンインゴット原料、スーパアロイ、アルミニウム合金用や鉄鋼用等の添加材等の用途に使用される。 <About Titanium Cobble>
The titanium cobble 41 obtained as described above is used for applications such as titanium ingot raw materials, super alloys, additives for aluminum alloys, steels, and the like.
以下、本開示に係る他の実施形態について詳述する。なお、これらの実施形態の説明において、実施形態1と同じ部分については同じ符号を付して詳細な説明を省略する。 (Other embodiments)
Hereinafter, other embodiments according to the present disclosure will be described in detail. In the description of these embodiments, the same parts as those in the first embodiment are denoted by the same reference numerals, and detailed description thereof is omitted.
11 スクラップ材
21 第1破砕機
23 第2破砕機
24 第1ふるい機(ふるい機)
25 第1磁選機
27 集塵機
27b 収集部
28 第2磁選機
29 第2ふるい機
30 第2コンベア装置(コンベア装置)
41 チタンコブル
42 微小チタンコブル
43 小チタンコブル
241 第1メッシュ(上側のメッシュ材)
242 第2メッシュ(下側のメッシュ材)
243 底部
410 微粉塵
411 大粒子
412 中粒子
413 小粒子
S1 準備工程
S2 第1破砕工程
S3 第2破砕工程
S4 集塵工程
S5 第1分級工程
S6 第1磁選工程
S7 リターン工程
S8 収集工程
S9 第2磁選工程
S10 第2分級工程 1 Manufacturing equipment (Titanium cobble manufacturing equipment)
11
25 1st
41
242 2nd mesh (lower mesh material)
243 Bottom 410
Claims (9)
- 金属チタンを50質量%以上含有するスクラップ材を準備する準備工程と、
前記スクラップ材を第1破砕機で粗破砕する第1破砕工程と、
前記第1破砕工程で粗破砕された前記スクラップ材を第2破砕機で粉砕する第2破砕工程と、
前記第2破砕工程において生じた前記スクラップ材の微粉塵を集塵する集塵工程と、
前記第2破砕工程において生じた前記スクラップ材の粉砕生成物を、所定の粒径範囲内の粒径を有する中粒子と、該粒径範囲を超える粒径を有する大粒子と、該粒径範囲よりも小さい粒径を有する小粒子とに分級する第1分級工程とを備えた
ことを特徴とするチタンコブルの製造方法。 A preparation step of preparing a scrap material containing 50% by mass or more of metal titanium;
A first crushing step of roughly crushing the scrap material with a first crusher;
A second crushing step of crushing the scrap material roughly crushed in the first crushing step with a second crusher;
A dust collection step of collecting fine dust of the scrap material generated in the second crushing step;
The pulverized product of the scrap material generated in the second crushing step includes medium particles having a particle size within a predetermined particle size range, large particles having a particle size exceeding the particle size range, and the particle size range. And a first classifying step of classifying the particles into smaller particles having a smaller particle size. - 請求項1において、
前記スクラップ材は、板材、チューブ材、サイドトリミング材、及び打ち抜き材の群から選ばれる少なくとも1種であり、
前記スクラップ材は、厚さ3mm以下、長さ1m以下の廃材である
ことを特徴とするチタンコブルの製造方法。 In claim 1,
The scrap material is at least one selected from the group of a plate material, a tube material, a side trimming material, and a punching material,
The scrap material is a scrap material having a thickness of 3 mm or less and a length of 1 m or less. - 請求項1又は請求項2において、
前記第1破砕機は二軸破砕機であり、
前記第2破砕機はハンマーミルである
ことを特徴とするチタンコブルの製造方法。 In claim 1 or claim 2,
The first crusher is a biaxial crusher;
The titanium cobble manufacturing method, wherein the second crusher is a hammer mill. - 請求項1~3のいずれか1項において、
前記中粒子の中から磁性を帯びたものを取り除く第1磁選工程と、
前記大粒子を前記第2破砕工程にリターンするためのリターン工程とを備えた
ことを特徴とするチタンコブルの製造方法。 In any one of claims 1 to 3,
A first magnetic separation step of removing the magnetic particles from the medium particles;
And a return process for returning the large particles to the second crushing process. - 請求項1~4のいずれか1項において、
前記集塵工程で集塵した前記微粉塵と前記小粒子とを集める収集工程と、
前記微粉塵と前記小粒子の集合物の中から磁性を帯びたものを取り除く第2磁選工程と、
前記集合物を少なくとも2種以上に分級する第2分級工程とを備えた
ことを特徴とするチタンコブルの製造方法。 In any one of claims 1 to 4,
A collecting step of collecting the fine dust and the small particles collected in the dust collecting step;
A second magnetic separation process for removing magnetism from the aggregate of the fine dust and the small particles;
And a second classifying step of classifying the aggregate into at least two types. - 請求項1~5のいずれか1項において、
前記所定の粒径範囲は3mm以上50mm以下である
ことを特徴とするチタンコブルの製造方法。 In any one of claims 1 to 5,
The method for producing titanium cobbles, wherein the predetermined particle size range is 3 mm or more and 50 mm or less. - 金属チタンを50質量%以上含有するスクラップ材を粗破砕する第1破砕機と、
前記第1破砕機で粗破砕された前記スクラップ材を粉砕する第2破砕機と、
前記第2破砕機による前記スクラップ材の粉砕時に生じる微粉塵を集塵する集塵機と、
前記第2破砕機による前記スクラップ材の粉砕により生じた粉砕生成物を、所定の粒径範囲内の粒径を有する中粒子と、該粒径範囲を超える粒径を有する大粒子と、該粒径範囲よりも小さい粒径を有する小粒子とに分級するふるい機とを備えた
ことを特徴とするチタンコブルの製造装置。 A first crusher for roughly crushing scrap material containing 50 mass% or more of metal titanium;
A second crusher for crushing the scrap material roughly crushed by the first crusher;
A dust collector that collects fine dust generated when the scrap material is pulverized by the second crusher;
The pulverized product produced by pulverizing the scrap material by the second crusher includes medium particles having a particle size within a predetermined particle size range, large particles having a particle size exceeding the particle size range, and the particles. An apparatus for producing a titanium cobble, comprising: a sieving machine for classifying into small particles having a particle size smaller than a diameter range. - 請求項7において、
前記中粒子の中から磁性を帯びたものを取り除く第1磁選機と、
前記大粒子を前記第2破砕機にリターンするためのコンベア装置とを備えたことを特徴とするチタンコブルの製造装置。 In claim 7,
A first magnetic separator that removes magnetism from the medium particles;
A titanium cobble manufacturing apparatus, comprising: a conveyor device for returning the large particles to the second crusher. - 請求項7又は請求項8において、
前記ふるい機は、異なる孔径の2種類のメッシュ材を上下2段に備えた振動ふるい機であり、
上側のメッシュ材の孔径は50mmであり、
下側のメッシュ材の孔径は3mmであり、
前記粉砕生成物は前記上側のメッシュ材上に配置されるものである
ことを特徴とするチタンコブルの製造装置。 In claim 7 or claim 8,
The sieve is a vibrating sieve equipped with two types of mesh materials with different pore sizes in upper and lower stages,
The hole diameter of the upper mesh material is 50 mm,
The hole diameter of the lower mesh material is 3 mm,
The said crushing product is arrange | positioned on the said upper mesh material, The manufacturing apparatus of the titanium cobble characterized by the above-mentioned.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB1912383.5A GB2573257B (en) | 2018-02-27 | 2019-02-21 | Method and machine for producing titanium cobbles |
US16/483,355 US10967386B2 (en) | 2018-02-27 | 2019-02-21 | Method and machine for producing titanium cobbles |
KR1020197025331A KR102137280B1 (en) | 2018-02-27 | 2019-02-21 | Manufacturing method and apparatus for titanium coble |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2018033414A JP6469912B1 (en) | 2018-02-27 | 2018-02-27 | Titanium cobble manufacturing method and manufacturing apparatus |
JP2018-033414 | 2018-02-27 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2019167804A1 true WO2019167804A1 (en) | 2019-09-06 |
Family
ID=65356166
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2019/006624 WO2019167804A1 (en) | 2018-02-27 | 2019-02-21 | Titanium cobble manufacturing method and manufacturing device |
Country Status (5)
Country | Link |
---|---|
US (1) | US10967386B2 (en) |
JP (1) | JP6469912B1 (en) |
KR (1) | KR102137280B1 (en) |
GB (1) | GB2573257B (en) |
WO (1) | WO2019167804A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112221960A (en) * | 2020-09-23 | 2021-01-15 | 江西东坚农业发展有限公司 | A screen scarifier for rice processing |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112169990B (en) * | 2019-07-02 | 2023-10-24 | 重庆市易特杰机械制造有限公司 | Dust-free crushing workstation and use method thereof |
BE1028041B1 (en) * | 2020-02-10 | 2021-09-06 | Capiau Recycling Nv | METHOD AND DEVICE FOR SEPARING MIXED ALUMINUM WASTE |
KR102431948B1 (en) * | 2020-05-08 | 2022-08-12 | (주)동아특수금속 | Manufacturing process technology of high quality-titanium cobble using titanium scrap |
CN111659700A (en) * | 2020-06-10 | 2020-09-15 | 江苏科盈选煤技术有限公司 | Separation device and method for lithium battery recovery |
CN113070145A (en) * | 2021-03-29 | 2021-07-06 | 江苏中宏环保科技有限公司 | Fine rubber powder production line |
CN115007444B (en) * | 2022-06-01 | 2023-06-23 | 安徽巢湖旺农业科技有限公司 | Environment-friendly sling type cloth bag dust removal process applied to grain processing |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0568948A (en) * | 1991-09-11 | 1993-03-23 | Ishikawajima Harima Heavy Ind Co Ltd | Classification apparatus and crushing equipment equipped with the same |
JP2001149911A (en) * | 1999-11-30 | 2001-06-05 | Ishikawajima Harima Heavy Ind Co Ltd | Processing method of waste gypsum board and apparatus therefor |
JP2002115005A (en) * | 2000-10-05 | 2002-04-19 | Daido Steel Co Ltd | METHOD FOR PRODUCING Ti OR Ti ALLOY POWDER USING Ti OR Ti ALLOY SCRAP AS RAW MATERIAL |
JP2008279422A (en) * | 2007-05-11 | 2008-11-20 | Katsuhiro Ito | System and apparatus for converting asbestos-containing building material into non-asbestos building material |
JP2009061357A (en) * | 2007-09-04 | 2009-03-26 | Kotobuki Giken Kogyo Kk | Apparatus and method for manufacturing sand, and sand |
JP2010234223A (en) * | 2009-03-31 | 2010-10-21 | Hitachi Zosen Corp | Waste disposal facility |
JP2017140555A (en) * | 2016-02-08 | 2017-08-17 | 株式会社エコネコル | Method and apparatus for recovering noble metal from incineration ash |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS497284B1 (en) | 1970-07-14 | 1974-02-19 | ||
US3905556A (en) * | 1974-05-20 | 1975-09-16 | Air Prod & Chem | Method and apparatus for recovery of metals from scrap |
US4416688A (en) * | 1980-09-02 | 1983-11-22 | Raymond Kaiser Engineers, Inc. | Direct reduction of ores and concentration of metallic values |
US4363722A (en) * | 1980-12-31 | 1982-12-14 | Suisman & Blumenthal, Incorporated | Process and apparatus for treating titanium machining scrap |
JP3369234B2 (en) | 1992-12-10 | 2003-01-20 | 同和鉱業株式会社 | Method for separating and recovering valuable resources from composite materials |
JP4608132B2 (en) * | 2001-05-30 | 2011-01-05 | 太平洋セメント株式会社 | Method for producing powdered cement dispersant |
JP2005036637A (en) * | 2003-06-27 | 2005-02-10 | Sadayoshi Yoshida | Drilling mud processing method and its processing apparatus |
JP2005068948A (en) * | 2003-08-28 | 2005-03-17 | Daiwa House Ind Co Ltd | Hinged door with door stopper function |
CN100445398C (en) * | 2004-08-02 | 2008-12-24 | 张维田 | Steel slag super fine powder processing technique and system |
JP2006104633A (en) * | 2004-10-08 | 2006-04-20 | Sanpo Shoko:Kk | Treatment system and method for recycling waste paper |
US7700038B2 (en) | 2005-03-21 | 2010-04-20 | Ati Properties, Inc. | Formed articles including master alloy, and methods of making and using the same |
US8109392B2 (en) * | 2005-08-29 | 2012-02-07 | Airstream Recycling Forces Pty Ltd | Apparatus and method for removing impurities in crushed recycled material |
JP4907284B2 (en) | 2006-09-28 | 2012-03-28 | 住友大阪セメント株式会社 | Method for processing ferrous waste materials |
AU2008241422B2 (en) * | 2007-04-18 | 2012-05-03 | Thomas A. Valerio | Method and system for sorting and processing recycled materials |
JP5707051B2 (en) * | 2010-04-16 | 2015-04-22 | 純二 多田 | Waste material treatment equipment |
JP5513435B2 (en) | 2011-04-13 | 2014-06-04 | 株式会社アビヅ | Manufacturing method of secondary materials for steel |
JP6011327B2 (en) * | 2012-12-27 | 2016-10-19 | 新日鐵住金株式会社 | Vibrating sieve device and cleaning method thereof |
CN108823412B (en) | 2018-06-20 | 2020-02-11 | 河南明泰铝业股份有限公司 | Processing and production process of secondary aluminum |
-
2018
- 2018-02-27 JP JP2018033414A patent/JP6469912B1/en active Active
-
2019
- 2019-02-21 US US16/483,355 patent/US10967386B2/en active Active
- 2019-02-21 GB GB1912383.5A patent/GB2573257B/en active Active
- 2019-02-21 KR KR1020197025331A patent/KR102137280B1/en active IP Right Grant
- 2019-02-21 WO PCT/JP2019/006624 patent/WO2019167804A1/en active Application Filing
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0568948A (en) * | 1991-09-11 | 1993-03-23 | Ishikawajima Harima Heavy Ind Co Ltd | Classification apparatus and crushing equipment equipped with the same |
JP2001149911A (en) * | 1999-11-30 | 2001-06-05 | Ishikawajima Harima Heavy Ind Co Ltd | Processing method of waste gypsum board and apparatus therefor |
JP2002115005A (en) * | 2000-10-05 | 2002-04-19 | Daido Steel Co Ltd | METHOD FOR PRODUCING Ti OR Ti ALLOY POWDER USING Ti OR Ti ALLOY SCRAP AS RAW MATERIAL |
JP2008279422A (en) * | 2007-05-11 | 2008-11-20 | Katsuhiro Ito | System and apparatus for converting asbestos-containing building material into non-asbestos building material |
JP2009061357A (en) * | 2007-09-04 | 2009-03-26 | Kotobuki Giken Kogyo Kk | Apparatus and method for manufacturing sand, and sand |
JP2010234223A (en) * | 2009-03-31 | 2010-10-21 | Hitachi Zosen Corp | Waste disposal facility |
JP2017140555A (en) * | 2016-02-08 | 2017-08-17 | 株式会社エコネコル | Method and apparatus for recovering noble metal from incineration ash |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112221960A (en) * | 2020-09-23 | 2021-01-15 | 江西东坚农业发展有限公司 | A screen scarifier for rice processing |
Also Published As
Publication number | Publication date |
---|---|
US10967386B2 (en) | 2021-04-06 |
GB201912383D0 (en) | 2019-10-16 |
US20210008568A1 (en) | 2021-01-14 |
JP6469912B1 (en) | 2019-02-13 |
KR102137280B1 (en) | 2020-07-23 |
GB2573257A (en) | 2019-10-30 |
JP2019147108A (en) | 2019-09-05 |
GB2573257B (en) | 2021-04-14 |
KR20190107733A (en) | 2019-09-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6469912B1 (en) | Titanium cobble manufacturing method and manufacturing apparatus | |
JP2000051830A (en) | Method for treating shredder dust | |
JPH10137610A (en) | Method for sorting and crushing material unsuitable for crushing and crushing apparatus therefor | |
US7478770B2 (en) | Mechanical granulation process | |
JPH0889932A (en) | Method and device for treatment of waste | |
JP2019153561A (en) | Method for processing lithium ion battery waste | |
JP2004000871A (en) | System for treating waste and method for treating waste dry cell | |
JP6676000B2 (en) | Method for grinding printed circuit board waste and method for recovering valuable metal from printed circuit board waste | |
JP2019037944A (en) | Printed circuit board scrap crushing device and printed circuit board scrap crushing method | |
JP2017154083A (en) | Crusher having striking member | |
JP6623127B2 (en) | Method and apparatus for producing reduced iron | |
JP5488008B2 (en) | Contamination separator | |
JP2019171267A (en) | Device for and method of treating waste lithium-ion battery | |
JP6846972B2 (en) | How to process printed circuit boards with parts and how to recover valuable metals from printed circuit boards with parts | |
EP4284615A1 (en) | Method and system for recycling wind turbine blades | |
CN206810428U (en) | A kind of titanium carbon alloy car considers recycle device to be worth doing | |
JP4813051B2 (en) | Reusable plastic production method | |
JP6139474B2 (en) | Recycling method and recycling system | |
US20240009682A1 (en) | Recovery of valuable components from a waste stream | |
Hesham et al. | Redesign and manufacture an impact crusher hammer mill using advanced iron casting | |
JP2004267821A (en) | Waste treatment apparatus | |
JP6586210B2 (en) | Method for producing chromium for powder metallurgy | |
JP4907284B2 (en) | Method for processing ferrous waste materials | |
JP2022022907A (en) | Method for producing high-purity silicon powder, high-purity silicon powder and system for producing high-purity silicon powder | |
CN206597623U (en) | A kind of graphite crushing system of multi-stage crushing for machining graphite |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
ENP | Entry into the national phase |
Ref document number: 20197025331 Country of ref document: KR Kind code of ref document: A |
|
ENP | Entry into the national phase |
Ref document number: 201912383 Country of ref document: GB Kind code of ref document: A Free format text: PCT FILING DATE = 20190221 |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 19761708 Country of ref document: EP Kind code of ref document: A1 |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
122 | Ep: pct application non-entry in european phase |
Ref document number: 19761708 Country of ref document: EP Kind code of ref document: A1 |